T. Lu et al.
the results of the oxidation over the THICA/MnO2 catalytic system in
various solvents. After a series of experiments, PEG1000–DAIL proves
to be the best solvent. And in traditional solvent acetic acid or ace-
tonitrile the conversion and selectivity are both lower under com-
parable conditions.[8] Poor conversion is obtained when the
reaction is performed in dichloromethane.[9] The catalytic activities
of THICA are not encouraged in PEG-1000-based dicationic ionic liq-
uid (PEG1000–DIL) due to its lack of acidity. Other PEG-based dica-
tionic acidic ionic liquids were also tested, but lower conversions
and selectivities are obtained.
In order to obtain further insight into the reaction under investi-
gation, the influence of reaction time and temperature on the cat-
alytic performance of THICA/MnO2 was investigated (Fig. 1). The
conversion or selectivity curves as a function of reaction time are
similar no matter which temperature was used. The reaction speed
sharply increases in initial 8 h, and then the oxidation proceeds
smoothly during 8–12 h, but the conversion and selectivity are
practically steady at 99% after 12 h. A reaction time of 12 h is con-
sidered as a preferable reaction time. The reaction temperature was
Scheme 1. Preparation of PEG1000–DAIL.
General Procedure for Oxidation
THICA was prepared using a literature procedure.[7] 1H NMR (DMSO-
d6, δ, ppm): 11.03 (s, 3H). 13C NMR (DMSO-d6, δ, ppm): 146.6. IR
(cmÀ1): 3539, 3166, 2827, 1720, 1433, 1211, 1010, 701.
PEG1000–DAIL was prepared using a procedure given in the liter-
ature (Scheme 1).[16] 1H NMR (D2O, δ, ppm): 2.15 (t, 4H, J = 7 Hz, 2 ×
CH2), 2.77 (m, 4H, 2 × CH2), 3.45–3.66 (m, 90.3H, (OCH2CH2)n), 3.74
(4H, 2 × CH2), 4.21–4.30 (8H, 4 × NCH2), 7.41 (s, 4H, 4 × CH), 8.71
(s, 2H, 2 × CH). 13C NMR (D2O, δ, ppm): 25.2, 47.7, 47.9, 49.1, 68.6,
68.7, 69.6, 122.3, 123.1, 136.0. IR (cmÀ1): 3849, 3400, 3020, 2883,
1732, 1591, 1456, 1431, 1377, 1122, 1109, 972, 883, 798, 677, 577.
The substrate (5 × 10À3 mol), PEG1000–DAIL (2.8 × 10À5 mol),
THICA (3.0 × 10À4 mol, 6 mol%) and MnO2 (2.0 × 10À4 mol, 4 mol
%) were placed in a three-necked flask. Oxygen was bubbled into
the flask at a flow rate of 20 ml minÀ1. The reaction mixture was
stirred at a specific temperature for a specific time, and the reaction
progress was monitored using HPLC. After completion of the reac-
tion, the mixture was cooled to room temperature and extracted
with ether a few times. After concentration of the ether solution,
the products were taken for HPLC measurement and PEG1000–DAIL
was reused without any treatment.
Table 1. Oxidation of toluene with various amounts of THICA/MnO2a
Entry
THICA
(mol%)
MnO2
(mol%)
Conversion
(%)b
Selectivity
(%)b
1
2
3
4
5
6
7
8
9
6
6
0
3
3
6
8
6
8
4
0
4
2
4
2
4
6
6
98.8
50.6
30.2
42.6
67.1
74.3
99.0
98.8
99.1
99.0
58.1
52.4
64.1
90.4
82.5
99.0
99.2
99.0
aReaction conditions: 5 × 10À3 mol toluene, 2.8 × 10À5 mol PEG1000
DAIL, 80°C, 12 h.
bConversion and selectivity of products were estimated from the peak
–
areas based on the internal standard technique using HPLC.
Results and Discussion
Influence of Reaction Conditions on Oxidation of Toluene with
THICA/MnO2
Table 2. Influence of solvent in oxidation catalyzed by THICA/MnO2a
The initial oxidation of toluene as a model substrate was investi-
gated using various amounts of THICA and MnO2 in PEG1000–DAIL
at 80°C for 12 h (Table 1). In the study, 6 mol% THICA and 4 mol%
MnO2 exert a better effect on the oxidation, affording 98.8% con-
version and 99.0% selectivity of benzoic acid (Table 1, entry 1). In
sharp contrast, the conversion is 50.6% when only using THICA as
catalyst. And MnO2 alone, realizing 30.2% conversion, is of low effi-
ciency (Table 1, entries 2 and 3). In comparison with the reaction
with 6 mol% THICA and 4% MnO2, the conversion of toluene mark-
edly decreases when the amounts of both catalytic components
are reduced by half. And the conversion is less than 75% when
the amount of one component is decreased to half in spite of
the other component being unchanged (Table 1, entries 4–6). On
the other hand, as the amount of either one component or both
the components is 1.5 times that of the original, the reaction
reaches a plateau at about 99.1% conversion and 99.2% selectivity
(Table 1, entries 7–9).
Entry
Solvent
Conversion (%)b
Selectivity (%)b
1c
2d
3d
4d
5c
6c
7c
8c
9c
10c
PEG1000–DAIL
CH2Cl2
98.8
61.4
96.5
88.3
90.2
97.1
97.7
85.5
25.8
11.6
99.0
52.2
95.1
87.6
89.0
98.3
98.5
90.4
43.9
32.3
HOAc
CH3CN
PEG1000–DIL
PEG400–DAIL
PEG600–DAIL
PEG2000–DAIL
[EMIm][Pro]
[BMIm]BF4
aReaction conditions: 5 × 10À3 mol toluene, 3.0 × 10À4 mol THICA, 2.0 ×
10À4 mol MnO2, 80°C, 12 h.
bConversion and selectivity of products were estimated from the peak
areas based on the internal standard technique using HPLC.
cSolvent: 2.8 × 10À5 mol.
dSolvent: 5 ml.
It is known from previous studies that the solvent has a great in-
fluence on the catalytic performance of THICA. Table 2 summarizes
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Appl. Organometal. Chem. (2015)